Each year more than a hundred million tons of polymer are produced worldwid
e in a variety of polymerization processes. Most of the polymerization reac
tions involved are highly exothermic so that very interesting and troubleso
me nonlinear dynamics arise routinely in these processes. In this paper, th
e key reaction parameters are examined for a variety of important polymers
and examples are provided illustrating the steady state multiplicity, susta
ined oscillations, and traveling waves which can arise in industrial reacto
rs. Among the reactors discussed are stirred tanks, loops, and fluidized be
ds. Some of the effects of imperfect mixing will also be demonstrated by ex
amples. (C) 1999 Elsevier Science Ltd. All rights reserved.